Process for the production of copper phthalocyanine pigment composition

Abstract: A process for the production of a copper phthalocyanine pigment composition comprising from 70 to 99 % by weight of a crude copper phthalocyanine and 30 to 1 % by weight of at least one phthalocyanine derivative, the process comprising dry milling all of the crude copper phthalocyanine and the phthalocyanine derivative in an amount of 0.5 to 10 % by weight of a final composition in the absence of a milling auxiliary until the content of an α-form phthalocyanine in the crude copper phthalocyanine is at least 20 % by weight, and adding and mixing the remaining phthalocyanine derivative to/with the dry-milled product.

Description: The present invention relates to a process for the production of a copper phthalocyanine pigment composition by a dry milling method. More specifically, it relates to a process for the production of a pigment composition, which comprises dry milling a crude copper phthalocyanine and a phthalocyanine derivative in the absence of a milling auxiliary and further mixing a phthalocyanine derivative with the milled product, and which shows stability with time when dispersed in a non-aqueous vehicle and shows less "strike-through" when used as an ink. A finely milled copper phthalocyanine has excellent fastness, a clear color tone and a high tinting strength, and it is hence widely used for various purposes in the industrial field of coloring materials. Since, however, a crude copper phthalocyanine produced by a general synthesis reaction is in the form of coarse crystal particles having a diameter of 1 to several tens µm, it is well known that such a crude copper phthalocyanine has insufficient pigment properties such as the tinting strength, hue, etc. which are required of pigments. For this reason, there are a variety of methods employed for converting it to a useful pigment form by finely milling a crude copper phthalocyanine to a size of approximately 0.01 to 0.5 µm. For obtaining a fine α-form pigment, there are a method in which a crude copper phthalocyanine is dissolved in concentrated sulfuric acid (acid pasting method) and a method in which a sulfuric acid salt is formed (acid slurry method). However, both these methods are industrially undesirable due to the use of a large amount of sulfuric acid and water and in view of the treatment of waste water. Further, the method for obtaining a fine β-form pigment is largely classified into (i) a dry milling method in which a crude copper phthalocyanine is milled in the presence of a milling auxiliary such as anhydrous sodium ferrocyanide or anhydrous barium chloride or a crude copper phthalocyanine is milled in the presence of a milling auxiliary and an organic liquid and then treated with an organic solvent and (ii) a wet milling method in which a crude copper phthalocyanine is milled with a mixing device (kneader) in the presence of a milling auxiliary such as sodium chloride and an organic liquid such as an alcohol or polyol. However, all of these methods require various steps and a large amount of energy, and are hence industrially undesirable. Further, α-form and β-form copper phthalocyanines obtained by the above methods have another problem in that a large amount of energy is further required for dissolving aggregates of their particles in a vehicle when an ink or a pigment is prepared therefrom. For overcoming the above problems, JP-B-55-6670 discloses that a pigment paste can be obtained by directly suspending a dry-milled product of a crude copper phthalocyanine in a solvent or resin solution used in an ink or a coating composition without converting the crude copper phthalocyanine into a pigment form. Further, JP-A-3-205458 discloses a copper phthalocyanine pigment composition obtained by dry milling a pigment derivative and a crude copper phthalocyanine in the absence of a milling auxiliary or by dry milling a crude copper phthalocyanine in the absence of a milling auxiliary and mixing the milled copper phthalocyanine with a pigment derivative. However, this pigment composition is insufficient in fluidity, tinting strength and stability with time when dispersed in a nonaqueous vehicle, and it is unsatisfactory in product quality since it shows "strike-through" when used for gravure printing on low-quality paper. It is an object of the present invention to provide a process for the production of a copper phthalocyanine pigment composition, in which a crude copper phthalocyanine can be converted to a pigment without a large amount of energy and the treatment of exhaust water. It is another object of the present invention to provide a process for the production of a copper phthalocyanine pigment composition, which can give a copper phthalocyanine pigment composition having excellent fluidity, tinting strength and stability with time when used in a coating composition or a printing ink. It is further another object of the present invention to provide a process for the production of a copper phthalocyanine pigment composition, which can give a copper phthalocyanine pigment composition which almost shows no "strike-through" when used for gravure printing on low-quality paper. According to the present invention, there is provided a process for the production of a copper phthalocyanine pigment composition which composition comprises from 70 to 99 % by weight of a crude copper phthalocyanine and 30 to 1 % by weight of at least one phthalocyanine derivative selected from phthalocyanine derivatives of the formulae (1) and (2), wherein M is H 2 , Al, Fe, Co, Ni, Cu or Zn, Pc is a phthalocyanine residue, X is -SO 2 -, -CH 2 -, -CH 2 NHCOCH 2 - or -CO-, each of R 1 and R 2 is independently a hydrogen atom or an alkyl group having 1 to 5 carbon atoms, or both R 1 and R 2 are constituents of one five-membered or six-membered heterocyclic ring which may contain a nitrogen atom or an oxygen atom and which may further contain, as a substituent, an alkyl group having 5 carbon atoms or less, m is an integer of 1 to 10, and n is an integer of 1 to 4, the process comprising dry milling the entirety of the crude copper phthalocyanine and the phthalocyanine derivative in an amount of 0.5 to 10 % by weight of a final composition in the absence of a milling auxiliary until the content of an α-form phthalocyanine in the crude copper phthalocyanine is at least 20 % by weight, and adding the remaining phthalocyanine derivative to the dry-milled product, and mixing. Specific examples of the phthalocyanine derivatives used in the present invention are as follows. CuPc-[SO 2 NH(CH 2 ) 3 N(C 2 H 5 ) 2 ] 2 CuPc-[SO 2 NH(CH 2 ) 3 N(CH 3 ) 2 ] 2 CuPc-[CH 2 NHCOCH 2 NH(CH 2 ) 3 N(C 4 H 9 ) 2 ] 3 CuPc-[CH 2 NH(CH 2 ) 5 N(C 2 H 5 ) 2 ] 2 CuPc-[CH 2 NH(CH 2 ) 4 (CH 3 ) 2 ] 3 CuPc-[CH 2 N(C 2 H 5 ) 2 ] 4 CuPc-[CONH(CH 2 ) 3 N(C 2 H 5 ) 2 ] 1 Concerning the amount of the phthalocyanine derivative, preferably, 70 to 99% by weight of the crude copper phthalocyanine and 0.5 to 10% by weight of the phthalocyanine derivative are dry milled in the absence of a milling auxiliary, and then 0.5 to 20% by weight of the phthalocyanine derivative is added to, and mixed with, the milled product. When the total amount of the phthalocyanine derivative is less than 1% by weight, the pigment dispersion is poor in tinting strength, gloss, fluidity and stability with time. The use of the phthalocyanine derivative in an amount of more than 30 by weight is uneconomical. The total amount of the phthalocyanine derivative is more preferably 3 to 15% by weight. The ratio of the phthalocyanine derivative to be added to the dry milled product to the phthalocyanine derivative dry milled together with the crude copper phthalocyanine is not especially limited but is typically from 1:1 to 5:1. In the process of the invention, the same phthalocyanine derivative as the phthalocyanine derivative dry milled together with the crude copper phthalocyanine can be added to the dry milled product. Alternatively, a phthalocyanine derivative different from the phthalocyanine derivative dry milled together with the crude copper phthalocyanine can be added to the dry milled product. Further, when a phthalocyanine derivative of the formula (1) is dry milled together with the crude copper phthalocyanine first, a phthalocyanine derivative of the formula (2) may be added, and mixed with, the dry milled product. When a phthalocyanine derivative of the formula (2) is dry milled together with the crude copper phthalocyanine first, a phthalocyanine derivative of the formula (1) may be added, and mixed with, the dry milled product. The crude copper phthalocyanine and the phthalocyanine derivative can be dry milled with any one of a ball mill, a vibration mill and an attriter at a milling temperature of 20 to 130°C. The pigment composition obtained by the above dry milling is a mixture of an α-form copper phthalocyanine and a β-form copper phthalocyanine. Typically, the crude copper phthalocyanine and the phthalocyanine derivative are dry milled until the dry milled product has an α-form content of 20 to 100% by weight, preferably 30 to 80% by weight. The present invention also provides a printing ink such as an offset ink or a gravure ink comprising a copper phthalocyanine pigment composition prepared according to the process of the invention. Also provided is a coating composition comprising a copper phthalocyanine pigment composition prepared according to the process of the invention. Typically, the coating composition further comprises a vehicle which is particularly preferably selected from nonaqueous vehicles containing an aromatic organic solvent such as toluene or xylene. The coating composition typically contains 1 to 20 by weight of the copper phthalocyanine pigment composition, 99 to 50% by weight of a vehicle for a coating composition and 0 to 30% by weight of other auxiliary and an extender pigment. The vehicle for a coating composition typically contains 80 to 20% by weight of a mixture of resins such as an acrylic resin, an alkyd resin, an epoxy resin, a polyurethane resin, a polyester resin and melamine resin and 60 to 10 by weight of a solvent such as a hydrocarbon, an alcohol, a ketone, an ether alcohol, an ether and an ester. The gravure ink typically contains 3 to 30% by weight of the copper phthalocyanine pigment composition obtained by the process of the present invention, 97 to 50% by weight of a vehicle for a gravure ink and 0 to 20% by weight of other auxiliary and an extender pigment. The vehicle for a gravure ink typically contains 10 to 50 % by weight of a mixture of resins such as lime rosin, rosin ester, a maleic acid resin, a polyamide resin, a vinyl resin, nitrocellulose, an ethylene-vinyl acetate copolymer resin, a urethane resin, a polyester resin and melamine resin and an alkyd resin and 30 to 80 % by weight of a solvent such as a hydrocarbon, an alcohol, a ketone, an ether alcohol, an ether and an ester. Examples The present invention will be explained more in detail hereinafter with reference to Examples, in which "part" stands for "part by weight" and "%" stands for "% by weight". Example 1 91 Parts of a crude copper phthalocyanine synthesized by a conventional method and 2 parts of a copper phthalocyanine derivative of the below-described formula were dry milled with an attriter at 60°C for 1.5 hours. The resultant dry milled product showed an α-form content of 68 % when analyzed by X-ray diffraction. Then, 7 parts of a copper phthalocyanine derivative of the below-described formula were mixed to give an intended copper phthalocyanine pigment composition. CuPc-[CH 2 NHCOCH 2 NH(CH 2 ) 3 N(C 4 H 9 ) 2 ] 3 Example 2 90 Parts of a crude copper phthalocyanine synthesized by a conventional method and 5 parts of a copper phthalocyanine derivative of the below-described formula were dry milled with an attriter at 40°C for 1 hour. The resultant dry milled product showed an α-form content of 63 % when analyzed by X-ray diffraction. Then, 5 parts of a copper phthalocyanine derivative of the below-described formula (3) were mixed to give an intended copper phthalocyanine pigment composition. CuPc-[SO 2 NH(CH 2 ) 3 N(C 2 H 5 ) 2 ] 2 Example 3 Example 2 was repeated except that the copper phthalocyanine derivative to be dry milled with the crude copper phthalocyanine was replaced with a copper phthalocyanine derivative of the formula (3). Example 4 Example 1 was repeated except that the temperature and time for the dry milling were changed to 95°C and 1 hour. The resultant dry milled product showed an α-form content of 32 % when analyzed by X-ray diffraction. Example 5 91 Parts of a crude copper phthalocyanine synthesized by a conventional method and 2 parts of an aluminum phthalocyanine derivative of the below-described formula were dry milled with an attriter at 40°C for 1 hour. The resultant dry milled product showed an α-form content of 66 % when analyzed by X-ray diffraction. Then, 7 parts of an aluminum phthalocyanine derivative of the below-described formula were mixed to give an intended phthalocyanine pigment composition. AlPc-[SO 2 NH(CH 2 ) 3 N(CH 3 ) 2 ] 2 Example 6 Example 5 was repeated except that the phthalocyanine derivative was replaced with a nickel phthalocyanine derivative of the below-described formula. NiPc-[CH 2 NH(CH 2 ) 5 N(C 2 H 5 ) 2 ] 2 Comparative Example 1 100 Parts of the same crude copper phthalocyanine as that used in Example 1 was dry milled with an attriter at 60°C for 1.5 hours. The resultant milled product showed an α-form content of 68 % when analyzed by X-ray diffraction. Comparative Example 2 91 Parts of a crude copper phthalocyanine synthesized by a conventional method and 9 parts of the same copper phthalocyanine derivative as that used in Example 1 were dry milled with an attriter at 60°C for 1.5 hours. The resultant dry milled product showed an α-form content of 68 % when analyzed by X-ray diffraction. Comparative Example 3 91 Parts of the milled product obtained in Comparative Example 1 was mixed with 9 parts of the same copper phthalocyanine derivative as that used in Example 1. Examples 7 - 10 Example 1 was repeated except that the amount of the copper phthalocyanine derivative to be dry milled together with the crude copper phthalocyanine and the amount of the copper phthalocyanine derivative to be mixed with the dry milled product were changed as shown in Table 1. Example Composition (part) α-form content (%) of dry milled Product Dry milled CuPc derivative mixed Crude CuPc CuPc derivative 7 95 2 3 69 8 93 3 4 67 9 90 3 7 67 10 85 5 10 65 (Evaluation methods) The pigment compositions obtained in Examples and the products obtained in Comparative Examples were evaluated as the following oil coating compositions and gravure inks. The oil coating composition was prepared by charging the pigment composition, the following components (1) and steel beads having a diameter of 3 mm into a glass bottle and dispersing them with a paint shaker for 90 minutes. The gravure ink was prepared by charging the pigment composition, the following components (2) and steel balls having a diameter of 5/8 inch to a magnetic pot and dispersed them with a jar mill for 15 hours. Components (1) Pigment composition 6 parts Alkyd resin varnish 56 parts Melamine resin varnish 28 parts Solvent 10 parts Components (2) Pigment composition 13 parts Lime rosin varnish 75 parts Solvent 12 parts The above-obtained pigment dispersions (oil coating compositions and gravure inks) were evaluated as follows. 1. Fluidity Immediately after the oil coating compositions and the gravure inks were prepared, each was measured for a viscosity with a Brookfield viscometer (supplied by Tokyo Keiki) at 6 rpm and 60 rpm. 2. Gloss 2-1. Oil coating composition An oil coating composition was spread on an art paper sheet with an applicator such that the coating had a wet thickness of 6 µm and baked in an oven at 120 to 130°C, and the coating was measured for 60° - 60° gloss with a glossmeter (supplied by Suga Testing Machine). "60° - 60°" means an incident angle and reflection angle of light. 2-2. Gravure ink A gravure ink was so adjusted by adding a solvent as to show a viscosity of 12 seconds when measured with a Zahn cup No. 3 (to be referred to as "printing viscosity" hereinafter), and then adjusted gravure ink was spread on a commercially available coat paper sheet (trade name; Henry SH) and a semi-coat paper sheet (trade name; Tokugra DX) with a bar coater such that the spread inks had a wet thickness of 6 µm, and each spread ink was measured for a gloss in the same manner as in the measurement of the oil coating composition. 3. Tinting strength 3-1. Oil coating composition An oil coating composition was mixed with a predetermined amount of a white coating composition, and the mixture was spread on an art paper sheet, baked and dried. The resultant coating was visually evaluated. 3-2. Gravure ink Each of a coat paper sheet and a semi-coat paper sheet on which a gravure ink was spread by the above method (2-2) were measured for a reflection density with a Gretag densitometer. 4. Strike-through of gravure ink The strike-through of a gravure ink spread on a semi-coat paper by the above method (2-2) was evaluated by measuring ΔE (color difference between a portion of the reverse side of the semi-coat paper on which the gravure ink was spread and a portion of the reverse side of the semi-coat paper on which no gravure ink was spread). 5. Stability of gravure ink with time A gravure ink which had been allowed to stand at 50°C for 1 week was measured for a viscosity at 6 rpm and 60 rpm with a Brookfield viscometer. Then, the gravure ink was adjusted to a printing viscosity, spread on a coat paper sheet and a semi-coat paper sheet with a bar coater such that the spread ink had a wet thickness of 6 µm, and measured for gloss (60° - 60°), reflection density (Gretag) and strike-trough state (ΔE). Table 2 shows the evaluation results of the oil coating compositions, Table 3 shows the evaluation results of the gravure inks immediately after they were prepared, and Table 4 shows the evaluation results of the gravure inks which had been allowed to stand for 1 week. Viscosity (cps) Gloss (%) Tinting strength (%) Ex. 1 280/270 87 standard Ex. 2 310/305 88 +2 Ex. 3 317/309 86 +1 Ex. 4 225/209 86 -2 Ex. 5 320/301 84 +1 Ex. 6 300/278 85 equivalent Ex. 7 305/288 86 -1 Ex. 8 230/218 90 equivalent Ex. 9 240/230 91 -1 Ex. 10 305/292 88 +2 CEx. 1 7,200/3,300 61 -15 CEx. 2 539/448 86 equivalent CEx. 3 295/282 84 -9 Viscosity (cPs) Gloss (%) Density Strike through of ink (ΔE) Coat paper Semi-coat paper Coat paper Semi-coat paper Ex. 1 98/92 56.5 21.6 2.75 2.58 7.6 Ex. 2 115/109 57.9 21.0 2.78 2.57 7.9 Ex. 3 120/112 56.7 21.8 2.76 2.56 8.0 Ex. 4 92/87 56.9 21.6 2.71 2.56 7.1 Ex. 5 128/119 56.5 19.8 2.74 2.53 7.7 Ex. 6 110/105 57.1 20.9 2.76 2.54 7.4 Ex. 7 117/108 55.5 20.8 2.73 2.53 8.0 Ex. 8 112/104 57.5 22.2 2.76 2.55 7.3 Ex. 9 101/94 58.1 22.0 2.77 2.57 7.5 Ex. 10 108/99 58.0 21.8 2.75 2.55 7.7 CEx. 1 450/390 47.1 10.2 2.05 1.88 15.1 CEx. 2 190/171 57.7 19.4 2.73 2.38 10.1 CEx. 3 110/104 53.7 21.0 2.64 2.48 7.9 Viscosity (cps) Gloss (%) Density Strike-through of ink (ΔE) Coat paper Semi-coat paper Coat paper Semi-coat paper Ex. 1 190/185 53.5 21.6 2.74 2.57 7.7 Ex. 2 230/201 54.3 20.3 2.76 2.52 8.1 Ex. 3 231/210 53.9 20.2 2.74 2.54 8.2 Ex. 4 183/171 54.2 21.8 2.71 2.52 7.3 Ex. 5 218/205 54.8 20.1 2.72 2.53 8.2 Ex. 6 230/211 53.2 19.9 2.73 2.51 8.3 Ex. 7 240/218 53.1 19.7 2.70 2.49 8.3 Ex. 8 202/190 55.0 21.8 2.73 2.54 7.7 Ex. 9 188/175 55.1 21.2 2.76 2.55 7.5 Ex. 10 203/192 54.9 20.2 2.74 2.53 7.9 CEx. 1 910/722 30.5 6.1 1.83 1.67 16.5 CEx. 2 670/534 49.2 16.1 2.61 2.11 13.1 CEx. 3 225/209 52.2 19.1 2.61 2.44 8.3 In the present invention, the phthalocyanine derivative and a crude copper phthalocyanine are dry milled together and then the phthalocyanine derivative is further added, whereby the phthalocyanine pigment particles in a vehicle can be controlled into a proper size and the phthalocyanine pigment composition can be effectively used in a coating composition and a printing ink. The pigment composition obtained according to the process of the present invention is excellent in fluidity, tinting strength and stability with time over, and freer from strike-through than, a composition obtained by merely adding a phthalocyanine derivative or dry milling the entirety of the phthalocyanine derivative together with a crude copper phthalocyanine.

Claims: A process for the production of a copper phthalocyanine pigment composition which composition comprises from 70 to 99 % by weight of a crude copper phthalocyanine and 30 to 1 % by weight of at least one phthalocyanine derivative selected from phthalocyanine derivatives of the formulae (1) and (2), wherein M is H 2 , Al, Fe, Co, Ni, Cu or Zn, Pc is a phthalocyanine residue, X is -SO 2 -, -CH 2 -, -CH 2 NHCOCH 2 - or -CO-, each of R 1 and R 2 is independently a hydrogen atom or an alkyl group having 1 to 5 carbon atoms, or both R 1 and R 2 are constituents of one five-membered or six-membered heterocyclic ring which may contain a nitrogen atom or an oxygen atom and which may further contain, as a substituent, integer of 1 to 10, and n is an integer of 1 to 4, the process comprising dry milling the entirety of the crude copper phthalocyanine and the phthalocyanine derivative in an amount of 0.5 to 10 % by weight of a final composition in the absence of a milling auxiliary until the content of an α-form phthalocyanine in the crude copper phthalocyanine is at least 20 % by weight, and adding the remaining phthalocyanine derivative to the dry-milled product, and mixing. A process according to claim 1, wherein the ratio of the phthalocyanine derivative to be added to the dry milled product to the phthalocyanine derivative dry milled together with the crude copper phthalocyanine is from 1:1 to 5:1. A process according to claims 1 or 2, wherein the same phthalocyanine derivative as the phthalocyanine derivative dry milled together with the crude copper phthalocyanine is added to the dry milled product. A process according to any preceding claim, wherein a phthalocyanine derivative different from the phthalocyanine derivative dry milled together with the crude copper phthalocyanine is added to the dry milled product. A process according to any preceding claim, wherein the crude copper phthalocyanine and the phthalocyanine derivative are dry milled until the dry milled product has an α-form content of 20 to 100 % by weight. A process according to any preceding claim, wherein the crude copper phthalocyanine and the phthalocyanine derivative are dry milled until the dry milled product has an α-form content of 30 to 80 % by weight. A printing ink comprising a copper phthalocyanine pigment composition prepared according to the process of any one of claims 1 to 6. A coating composition comprising a copper phthalocyanine composition prepared according to the process of any one of claims 1 to 6.

Inventors: KATO SHIGEKI, MURAMATSU YOSHIO, TSUJI KOSAKU, KATO, SHIGEKI, MURAMATSU, YOSHIO, TSUJI, KOSAKU, KATO, SHIGEKI, C/O TOYO INK MANUFACT. CO. LTD., MURAMATSU, YOSHIO, C/O TOYO INK MANUFACT. CO. LTD., TSUJI, KOSAKU, C/O TOYO INK MANUFACT. CO. LTD.
Applicants: TOYO INK MFG CO, TOYO INK MANUFACTURING CO., LTD.
Application year: 1994
Main classification: C09B67
IPC codes: C09B67, C09B47